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JPS6254013A - Method and apparatus for melting scrap - Google Patents

Method and apparatus for melting scrap

Info

Publication number
JPS6254013A
JPS6254013A JP60194227A JP19422785A JPS6254013A JP S6254013 A JPS6254013 A JP S6254013A JP 60194227 A JP60194227 A JP 60194227A JP 19422785 A JP19422785 A JP 19422785A JP S6254013 A JPS6254013 A JP S6254013A
Authority
JP
Japan
Prior art keywords
scrap
furnace body
furnace
combustion
melting
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP60194227A
Other languages
Japanese (ja)
Inventor
Takamitsu Yamada
山田 隆光
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP60194227A priority Critical patent/JPS6254013A/en
Publication of JPS6254013A publication Critical patent/JPS6254013A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/52Manufacture of steel in electric furnaces
    • C21C5/527Charging of the electric furnace
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Abstract

PURPOSE:To reduce cost and to improve productivity by subjecting the scrap in a furnace body to initial melting by an arc, storing a prescribed amt. of the molten scrap, blowing a carboneous material and oxygen into a molten steel and melting the remaining scrap by the combustion energy generated by the combustion of CO. CONSTITUTION:The scrap in one of the plural furnace bodies is initially melted by the arc and a prescribed amt. of the molten steel is stored in one furnace body by the initial melting. The carboneous material and oxygen are blown into the molten steel to generate the combustion energy by the combustion of CO. The remaining scrap in the one furnace body is melted by such combustion energy. The heating of the scrap in the other furnace body is executed by the combustion of the CO in the waste gas generated by the initial melting or the waste gas contg. the CO and the preheating of the scrap in the one furnace body is executed by the waste gas from the other furnace body.

Description

【発明の詳細な説明】 し産業上の利用分野] 本発明は、省電力化、省エネルギー化を図ると共に製鋼
コストの低減、生産性の向上を図り得るようにしたスク
ラップの溶解方法及び装置に関するものである。
[Detailed Description of the Invention] Field of Industrial Application] The present invention relates to a scrap melting method and apparatus that are capable of saving power and energy, reducing steel manufacturing costs, and improving productivity. It is.

[従来の技術] 通常の製鋼用アーク炉はスクラップの溶解エネルギーを
ほとんど電気エネルギーに頼り、補助エネルギーとして
一部を酸素バーナで供給している程度である。又省エネ
ルギ一対策として、第4図に示すように2炉交換システ
ムを採用してスクラップの加熱、溶解を交互に行うよう
にし、一方の炉本体aで生じた溶解時の排ガスを連結用
ダクトbを介して他方の炉本体Cに導入するようにし、
炉本体C内のスクラップdを予熱し、熱回収を行ってい
る。図中eは電極、fは排ガスダクト、(1,g+は炉
蓋である。
[Prior Art] Ordinary arc furnaces for steelmaking rely almost entirely on electrical energy for scrap melting energy, with only some supplementary energy being supplied by an oxygen burner. In addition, as an energy-saving measure, a two-furnace exchange system is adopted as shown in Figure 4, heating and melting the scrap alternately, and exhaust gas generated during melting in one furnace body a is transferred to the connecting duct. so that it is introduced into the other furnace body C via b,
The scrap d in the furnace body C is preheated and heat is recovered. In the figure, e is an electrode, f is an exhaust gas duct, and (1, g+ is a furnace lid.

[発明が解決しようとする問題点] しかしながら上述の製鋼用アーク炉にあっては、溶解エ
ネルギーを大部分電気エネルギーに依存しているため電
力消費量が大きく製鋼コストがアップする。又排ガスに
よるスクラップの予熱によって回収される熱は、炉本体
からの排ガスは温度変化が激しく且つ平均的に温度レベ
ルが低いため、通常高々5〜15%程度であり、更に、
炉本体a、bのプロフィルでは、排ガスダクトfが炉M
(J’に設けであるため排ガスは予熱用の炉本体すのス
クラップd内をショートパスし、対流電熱効果が良くな
い。
[Problems to be Solved by the Invention] However, in the above-mentioned arc furnace for steelmaking, the melting energy is largely dependent on electric energy, resulting in large power consumption and increased steelmaking costs. In addition, the heat recovered by preheating the scrap with exhaust gas is usually about 5 to 15% at most, because the exhaust gas from the furnace body has a large temperature change and an average low temperature level.
In the profiles of the furnace bodies a and b, the exhaust gas duct f is connected to the furnace M.
(Since it is installed at J', the exhaust gas takes a short path through the scrap d of the furnace main body for preheating, and the convection electric heating effect is not good.

本発明は上述の実情に鑑み、消費電力を低減させて省電
力及び省エネルギー並びにコストの低減を図ると共に生
産性の向上を図ることを目的としている。
In view of the above-mentioned circumstances, it is an object of the present invention to reduce power consumption, save power and energy, reduce costs, and improve productivity.

[問題点を解決するための手段] 本発明は炉本体内のスクラップをアークにより初期溶解
し、初期溶解により溶鋼が炉本体内に所定量溜ったら該
溶鋼中に炭材及び酸素を吹込んでCOの燃焼により燃焼
エネルギーを発生させ、該燃焼エネルギーで炉本体内の
残余のスクラップの溶解を行わせる構成を備え、且つ複
数の炉本体のうち一方の炉本体内のスクラップをアーク
により初期溶解し、初期溶解により溶鋼が一方の炉本体
内に所定但溜ったら該溶鋼中に炭材及び酸素を吹込んで
COの燃焼により燃焼エネルギーを発生させ、該燃焼エ
ネルギーで前記一方の炉本体内の残余のスクラップの溶
解を行わせ、前記初期溶解により発生した排ガス或いは
COを含む排ガス中のCOの燃焼により他方の炉本体中
のスクラップの加熱を行い、他方の炉本体からの排ガス
によりスクラップの予熱を行う構成を備えている。
[Means for Solving the Problems] The present invention involves initially melting the scrap in the furnace body using an arc, and when a predetermined amount of molten steel accumulates in the furnace body due to the initial melting, carbonaceous material and oxygen are injected into the molten steel to remove CO. is configured to generate combustion energy by combustion of the furnace body, and melt the remaining scrap in the furnace body with the combustion energy, and initially melt the scrap in one of the plurality of furnace bodies by an arc, When molten steel accumulates in a predetermined amount in one furnace body due to initial melting, carbonaceous material and oxygen are injected into the molten steel to generate combustion energy by combustion of CO, and the remaining scrap in the one furnace body is used to generate combustion energy. A configuration in which the scrap in the other furnace body is heated by the combustion of CO in the exhaust gas generated by the initial melting or the exhaust gas containing CO, and the scrap is preheated by the exhaust gas from the other furnace body. It is equipped with

[作  用] 本発明では、所定の炉本体中のスクラップのアークによ
る初期溶解の後に炭材及び酸素が溶鋼中に供給され、炭
材及び酸素の反応により生じるCOの燃焼熱により残っ
たスクラップの溶解が行われ、初期溶解時の排ガス及び
COを含む排ガス中のCOの燃焼熱により溶解の行われ
ていない炉本体のスクラップが高温或いは半溶解状態ま
で加熱が行われ、該加熱後の排ガスによりスクラップ予
熱槽内のスクラップの予熱が行われる。
[Function] In the present invention, carbonaceous material and oxygen are supplied into molten steel after the initial melting of scrap in a predetermined furnace body by an arc, and the remaining scrap is melted by the combustion heat of CO generated by the reaction of carbonaceous material and oxygen. Melting is performed, and the unmelted scrap of the furnace body is heated to a high temperature or semi-molten state by the combustion heat of CO in the exhaust gas and CO in the exhaust gas after the heating, and the exhaust gas after heating The scrap in the scrap preheating tank is preheated.

[実 施 例] 以下、本発明の実施例を添付図面を参照しつつ説明する
[Example] Hereinafter, an example of the present invention will be described with reference to the accompanying drawings.

第1図〜第3図は本発明の一実施例で、所要の間隔を置
いて配設した炉本体1a、 lbの上部テーパ一部は連
結用ダクト2により連結され、炉本体1a、 lb上下
部互に逆方向へ向けて突出させた張出し部3a、3bに
は、炉底出鋼口4a、 4bが設けられると共に排ガス
出口5a、 5bが設けられ、排ガス出口5a、 5b
に接続した排ガスダクト6a。
Figures 1 to 3 show an embodiment of the present invention, in which a portion of the upper taper of the furnace bodies 1a, lb arranged at a required interval is connected by a connecting duct 2, and the upper and lower parts of the furnace bodies 1a, lb are connected by a connecting duct 2. The overhanging parts 3a, 3b that project in mutually opposite directions are provided with furnace bottom tapping ports 4a, 4b, and are also provided with exhaust gas outlets 5a, 5b.
Exhaust gas duct 6a connected to.

6bは排ガスダクト7に接続され、排ガスダクト7から
は炉本体1a又は1bからの排ガスをスクラップ予熱槽
8に頂部から供給し得るようになっている。又炉本体1
a、 II)の上部空間はCOガス燃焼のため十分な広
さになっており、スクラップ予熱槽8下部からは排ガス
を排出し得るようになっている。
6b is connected to an exhaust gas duct 7, from which exhaust gas from the furnace body 1a or 1b can be supplied to the scrap preheating tank 8 from the top. Furnace body 1
The upper space of a, II) is large enough for CO gas combustion, and exhaust gas can be discharged from the lower part of the scrap preheating tank 8.

炉本体1a、lb間の略中間位置には、炉蓋着脱装置9
が配設されている。該炉蓋看1152装置9には、点X
を中心として水平方向へ旋回自在な枠体10及び該枠体
10に取付けられ、電極11を備えたアーク溶解用の炉
M12を昇降させる昇降装置(図示せず)等が設けられ
ている。
Approximately midway between the furnace bodies 1a and lb, there is a furnace cover attachment/detachment device 9.
is installed. The furnace cover 1152 device 9 has a point
A frame 10 is provided which can be rotated horizontally around the center, and a lifting device (not shown) attached to the frame 10 for lifting and lowering an arc melting furnace M12 provided with an electrode 11 is provided.

炉本体1a、 lbの左右に敷設したレール13a、1
3bには炉蓋着脱装置14a、 14bが炉本体1a、
1bに対して近接、離反し得るよう配設され、該炉蓋看
脱装置14a、 14bの枠体15a、 15bには、
加熱用の炉116a、16bを昇降ざぜる昇降装置(図
示せず)等が設けられている。
Rails 13a, 1 laid on the left and right sides of the furnace body 1a, lb
3b, the furnace lid attaching/detaching device 14a, 14b is attached to the furnace body 1a,
The frames 15a and 15b of the furnace cover removal devices 14a and 14b are arranged so as to be able to approach and move away from the furnace cover removal device 1b.
An elevating device (not shown) for elevating and lowering the heating furnaces 116a and 16b is provided.

図中17a、17bは炉本体1a、 lbの炉底に取付
けられた、コークス、石炭等の炭材及び酸素を吹込むた
めのノズル、18a、18b 、 19a、19bは炉
本体1a、lb側壁部に設けたバーナ、20a、 20
bは炉本体1a、 1b頂部に設けた酸素吹込み用のノ
ズル、21a、21bは炉116a、16bに設けた酸
素吹込用のノズル、22は連結用ダクト2に設けたバル
ブ、23a、23bは排ガスダクト6a、6bに設けた
バルブ、24はダクト7に設けたバルブ、25は電源ト
ランス、26a、 26bは炉本体1a、 lb内のス
クラップ、27は溶鋼である。
In the figure, 17a and 17b are nozzles installed on the bottom of the furnace body 1a and lb for injecting carbonaceous materials such as coke and coal and oxygen, and 18a, 18b, 19a and 19b are installed on the side wall of the furnace body 1a and lb. burner, 20a, 20
21a and 21b are nozzles for oxygen injection provided in the furnaces 116a and 16b, 22 is a valve provided in the connecting duct 2, and 23a and 23b are Valves installed in the exhaust gas ducts 6a and 6b, 24 a valve installed in the duct 7, 25 a power transformer, 26a and 26b scraps in the furnace body 1a and 1b, and 27 molten steel.

例えば、炉本体1a内でスクラップ26aを溶解し、炉
本体1b内でスクラップ26bを加熱し、スクラップ予
熱槽8でスクラップを予熱する場合には、炉蓋着脱装置
9を第3図において時計方向へ回動させ炉本体1aを炉
i12により遮蔽し、電極11を炉本体1a内に挿入し
、炉蓋着脱装置14bを炉本体1b側へ前進させて炉本
体1bを炉M16bにより密閉し、バルブ22.23b
、 24を開き、バルブ23aを閉止させ、電源トラン
ス25により電極11に通電を行い、炉本体1a内のス
クラップ26aのアークによる溶解を開始する。この際
、バーナ18a、19aを併用しても良い。
For example, when scrap 26a is melted in the furnace body 1a, scrap 26b is heated in the furnace body 1b, and the scrap is preheated in the scrap preheating tank 8, the furnace lid attaching/detaching device 9 is moved clockwise in FIG. The furnace body 1a is rotated to be shielded by the furnace i12, the electrode 11 is inserted into the furnace body 1a, the furnace lid attachment/detachment device 14b is advanced toward the furnace body 1b side, the furnace body 1b is sealed by the furnace M16b, and the valve 22 .23b
, 24 is opened, the valve 23a is closed, and the electrode 11 is energized by the power transformer 25 to start melting the scrap 26a in the furnace body 1a by arc. At this time, burners 18a and 19a may be used together.

スクラップ26aの溶解により発生したガスは連結用ダ
クト2から炉本体1b内に炉頂部より導入され、スクラ
ップ26bを加熱後、張出し部3bより排ガスダクト6
bに排出され、排ガスダクト6b、・7からスクラップ
予熱槽8に導入され、該予熱槽8内のスクラップを予熱
後図示してないブロワに吸引されて外部へ排出される。
The gas generated by melting the scrap 26a is introduced into the furnace body 1b from the connecting duct 2 from the top of the furnace, and after heating the scrap 26b, is passed through the overhang 3b into the exhaust gas duct 6.
b, and introduced into the scrap preheating tank 8 through the exhaust gas ducts 6b, 7, and after preheating the scrap in the preheating tank 8, it is sucked by a blower (not shown) and discharged to the outside.

アーク電力投入後、炉本体1a内のスクラップ26bが
約30%程度溶解し、溶鋼27が炉底に溜ったら、電源
トランス25を遮断してアークによる溶解をやめ、炉蓋
着脱装置9により炉蓋12を炉本体1aから撤去して待
機位置まで移動させ、炉蓋着脱装置14aを作動させて
炉116aにより炉本体1a上部を遮蔽させ、溶鋼27
中にノズル17aより炭材と酸素を吹込み、スクラップ
26aの溶解を行う。炭材と酸素の吹込みにより発生し
たCOガスは、一部はノズル20a、21a等から炉本
体1a内に吹込んだ酸素で燃焼し、その燃焼エネルギー
はスクラップ26aの溶解、溶鋼27の昇温及び精錬に
奇与し、残りのCOを含んだ排ガスは、連結用ダクト2
から炉本体1b内に導入され、スクラップ26bを高温
又は半溶解状態まで加熱し、しかる後炉本体1bから排
出されてスクラップ予熱槽8へ導入され、スクラップの
予熱に利用される。
After the arc power is turned on, when approximately 30% of the scrap 26b in the furnace body 1a is melted and molten steel 27 accumulates at the bottom of the furnace, the power transformer 25 is shut off to stop melting by the arc, and the furnace lid is removed by the furnace lid attaching/detaching device 9. 12 is removed from the furnace body 1a and moved to the standby position, the furnace lid attaching/detaching device 14a is operated to shield the upper part of the furnace body 1a with the furnace 116a, and the molten steel 27 is removed from the furnace body 1a and moved to the standby position.
Carbon material and oxygen are blown into the inside from the nozzle 17a to melt the scrap 26a. The CO gas generated by injecting carbonaceous material and oxygen is partially combusted by the oxygen injected into the furnace body 1a from the nozzles 20a, 21a, etc., and the combustion energy is used to melt the scrap 26a and raise the temperature of the molten steel 27. The remaining CO-containing exhaust gas that has contributed to the refining process is transferred to the connecting duct 2.
The scrap 26b is introduced into the furnace body 1b and heated to a high temperature or semi-molten state, and then discharged from the furnace body 1b and introduced into the scrap preheating tank 8, where it is used for preheating the scrap.

而して、炉本体1a内のスクラップ26aが全組溶解し
て所定温度まで昇温したら炉本体1aでの溶解を停止し
、炉底出鋼口(図示せず)を開いて溶鋼を図示してない
取鍋に排出させる。又炉本体1aでの溶鋼の溶解、排出
が終了したら炉蓋着脱装置14a、14bにより炉11
6a、16bを炉本体la、 lbから撤去すると共に
炉蓋着脱装置9を第3図の反時計方向へ作動させ、炉蓋
12によって炉本体1bを遮蔽し、スクラップ予熱槽8
内のスクラップをクレーン或いは専用台車で炉本体1a
内に供給し、炉蓋着脱装置14aによって炉本体1aを
炉蓋16aで遮蔽し、スクラップ予熱槽8内にスクラッ
プを入れ、バルブ2.23a、z4を開き、バルブ23
bを閉止し、前述と同様にして炉本体1bでスクラップ
26bの溶解が、炉本体1aでスクラップ26aの加熱
がスクラップ予熱槽8でスクラップの予熱が、夫々行わ
れる。
When all the scraps 26a in the furnace body 1a have been melted and the temperature has risen to a predetermined temperature, the melting in the furnace body 1a is stopped, and the furnace bottom tapping port (not shown) is opened to draw the molten steel. Drain into a ladle. Furthermore, after the melting and discharging of molten steel in the furnace body 1a is completed, the furnace 11 is
6a and 16b are removed from the furnace bodies la and lb, and the furnace lid attachment/detachment device 9 is operated in the counterclockwise direction in FIG.
Remove the scraps from the furnace body 1a using a crane or a special trolley.
The furnace main body 1a is shielded with the furnace lid 16a by the furnace lid attaching/detaching device 14a, the scrap is put into the scrap preheating tank 8, the valves 2.23a and z4 are opened, and the valve 23 is
b is closed, and the scrap 26b is melted in the furnace body 1b, the scrap 26a is heated in the furnace body 1a, and the scrap is preheated in the scrap preheating tank 8 in the same manner as described above.

上述のように、スクラップを排ガスによりスクラップ予
熱槽8で予熱し、炉本体1a、lbのうち一方の炉本体
で他方の炉本体からの排ガス又はCOガスの燃焼によっ
て加熱し、他方の炉本体でアーク電力により初期溶解す
ると共に炭材燃料で残りのスクラップの溶解、昇温を行
うことにより、アーク電力投入時の電力消費量は150
KW!l/T程度となり、従来の電力消費量400〜5
00に聞/■に比較して著しく減少する。従って、製鋼
コストが減少し、生産性が向上する。
As mentioned above, scrap is preheated in the scrap preheating tank 8 using exhaust gas, heated in one of the furnace bodies 1a and lb by combustion of exhaust gas or CO gas from the other furnace body, and heated in the other furnace body. By performing initial melting with arc power and melting remaining scrap with carbonaceous fuel and raising temperature, power consumption when arc power is applied is 150%.
KW! It is about l/T, and the conventional power consumption is 400 to 5
It decreases significantly compared to 00/■. Therefore, steel manufacturing costs are reduced and productivity is improved.

なお、本発明は上述の実施例に限定されるちのではなく
、本体は1基でも実施できること、スクラップ予熱槽は
複数設けても実施し得ること、バーナはなくても良いこ
と、その伯、本発明の要旨を逸脱しない範囲内で種々変
更を加えjqること、等は勿論である。
It should be noted that the present invention is not limited to the above-mentioned embodiments, but also that it can be implemented with a single main body, that it can be implemented even with a plurality of scrap preheating tanks, that it does not require a burner, and that Of course, various changes may be made without departing from the spirit of the invention.

[発明の効果] 本発明のスクラップの溶解方法及び装置によれば、 <I>  電力エネルギーの多くを安価な炭材エネルギ
ーに代替させることができるため省電力化が可能となり
且つ生産コストを低減させることができる、 <n>  溶鋼中で発生したCOガスの顕熱を本システ
ム内で有効に利用できるため省エネルギーに貢献できる
、 <1>  炉本体上部から導入したガスを炉本体下部に
設けた張出し部から排出し得るようにしたため、スクラ
ップの加熱を効率良く行うことができる、 ■ 電力エネルギーの低減により小容量の変電設備で良
く、フリッカ等の公害を防止できる、等、種々の優れた
効果を奏し得る。
[Effects of the Invention] According to the scrap melting method and device of the present invention, <I> Much of the electrical energy can be replaced with inexpensive carbonaceous energy, making it possible to save power and reduce production costs. <n> Sensible heat of CO gas generated in molten steel can be effectively used within this system, contributing to energy saving. <1> Overhang provided at the bottom of the furnace body for gas introduced from the top of the furnace body. It has various excellent effects, such as the ability to heat scrap efficiently as it can be discharged from a It can be played.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図〜第3図は本発明の一実施例の説明図で、第1図
は一つの炉本体でアークによりスクラップを初期溶解し
その排ガスで伯の炉本体のスクラップを加熱し予熱槽の
スクラップを予熱する場合の説明図、第2図は一つの炉
本体でCOガスを酸素により燃焼させ燃焼エネルギーで
スクラップを溶解、昇温させ、排ガス中のCoを伯の炉
本体で酸素により燃焼させその燃焼エネルギニでスクラ
ップを高温又は半溶解状態まで加熱し予熱槽でスクラッ
プを予熱する場合の説明図、第3図は平面図、第4図は
従来例の説明図である。 図中1は炉本体、2は連結用ダクト、3a、 3bは張
出し部、6a、 6b、 7は排ガスダクト、8はスク
ラップ予熱槽、11は電極、17a、 17b、 20
a、 20b。 21a、21bはノズル、25は電源トランス、26a
、26t)はスクラップ、27は溶鋼を示す。
Figures 1 to 3 are explanatory diagrams of one embodiment of the present invention. Figure 1 shows the initial melting of scrap using an arc in one furnace body, and the exhaust gas used to heat the scrap in the furnace body. An explanatory diagram for preheating scrap. Figure 2 shows a method in which CO gas is combusted with oxygen in one furnace body, the scrap is melted and heated by the combustion energy, and Co in the exhaust gas is combusted with oxygen in the other furnace body. The combustion energy is used to heat the scrap to a high temperature or semi-molten state, and the scrap is preheated in a preheating tank. FIG. 3 is a plan view, and FIG. 4 is an explanatory diagram of a conventional example. In the figure, 1 is the furnace body, 2 is a connecting duct, 3a, 3b are overhanging parts, 6a, 6b, 7 are exhaust gas ducts, 8 is a scrap preheating tank, 11 is an electrode, 17a, 17b, 20
a, 20b. 21a and 21b are nozzles, 25 is a power transformer, 26a
, 26t) indicates scrap, and 27 indicates molten steel.

Claims (1)

【特許請求の範囲】 1)炉本体内のスクラップをアークにより初期溶解し、
初期溶解により溶鋼が炉本体内に所定量溜ったら該溶鋼
中に炭材及び酸素を吹込んでCOの燃焼により燃焼エネ
ルギーを発生させ、該燃焼エネルギーで炉本体内の残余
のスクラップの溶解を行わせることを特徴とするスクラ
ップの溶解方法。 2)複数の炉本体のうち一方の炉本体内のスクラップを
アークにより初期溶解し、初期溶解により溶鋼が一方の
炉本体内に所定量溜ったら該溶鋼中に炭材及び酸素を吹
込んでCOの燃焼により燃焼エネルギーを発生させ、該
燃焼エネルギーで前記一方の炉本体内の残余のスクラッ
プの溶解を行わせ、前記初期溶解により発生した排ガス
或いはCOを含む排ガス中のCOの燃焼により他方の炉
本体中のスクラップの加熱を行い、他方の炉本体からの
排ガスによりスクラップの予熱を行うことを特徴とする
スクラップの溶解方法。 3)炭材及び酸素吹込みノズルを備え頂部側を連結用ダ
クトで接続されしかも炉頂部を電極を備えた炉蓋或いは
電極のない炉蓋で遮蔽し得るようにした複数の炉本体と
、各炉本体炉底部の張出し部に接続され排ガスをスクラ
ップ予熱槽に供給し得るようにしたダクトとを設けたこ
とを特徴とするスクラップの溶解装置。
[Claims] 1) Initial melting of scrap in the furnace body using an arc,
When a predetermined amount of molten steel accumulates in the furnace body due to initial melting, carbonaceous material and oxygen are injected into the molten steel to generate combustion energy by burning CO, and the remaining scrap in the furnace body is melted with this combustion energy. A scrap melting method characterized by: 2) The scrap in one of the multiple furnace bodies is initially melted using an arc, and when a predetermined amount of molten steel accumulates in one of the furnace bodies due to the initial melting, carbonaceous material and oxygen are injected into the molten steel to remove CO. Combustion energy is generated by combustion, the remaining scrap in the one furnace body is melted by the combustion energy, and the other furnace body is melted by combustion of CO in the exhaust gas or CO-containing exhaust gas generated by the initial melting. A scrap melting method characterized by heating the scrap inside and preheating the scrap with exhaust gas from the other furnace body. 3) A plurality of furnace bodies equipped with carbon material and oxygen blowing nozzles, connected at the top side by a connecting duct, and in which the top of the furnace can be shielded with a furnace lid equipped with an electrode or a furnace lid without an electrode; 1. A scrap melting device characterized by being provided with a duct connected to an overhanging part of the bottom of the furnace body and capable of supplying exhaust gas to a scrap preheating tank.
JP60194227A 1985-09-03 1985-09-03 Method and apparatus for melting scrap Pending JPS6254013A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60194227A JPS6254013A (en) 1985-09-03 1985-09-03 Method and apparatus for melting scrap

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60194227A JPS6254013A (en) 1985-09-03 1985-09-03 Method and apparatus for melting scrap

Publications (1)

Publication Number Publication Date
JPS6254013A true JPS6254013A (en) 1987-03-09

Family

ID=16321071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60194227A Pending JPS6254013A (en) 1985-09-03 1985-09-03 Method and apparatus for melting scrap

Country Status (1)

Country Link
JP (1) JPS6254013A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5626686A (en) * 1979-08-12 1981-03-14 Takefu Tokushu Kozai Kk Production for clad material
JPS5938582A (en) * 1982-08-26 1984-03-02 マンネスマン・アクチエンゲゼルシヤフト Dissolving device for steel with two furnace vessel
JPS6032873U (en) * 1983-08-09 1985-03-06 パイオニア株式会社 Color band amplifier circuit

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5626686A (en) * 1979-08-12 1981-03-14 Takefu Tokushu Kozai Kk Production for clad material
JPS5938582A (en) * 1982-08-26 1984-03-02 マンネスマン・アクチエンゲゼルシヤフト Dissolving device for steel with two furnace vessel
JPS6032873U (en) * 1983-08-09 1985-03-06 パイオニア株式会社 Color band amplifier circuit

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